A mini scale batch reactor for the production of palm‑based polyol
An investigation on a batch production of palm kernel oil polyol (PKO-p) was conducted via esterification and condensation. The process design was thoroughly studied as a preliminary step for future upscaling. The process variables included necessity of vacuum pump, controlling of heating rate, reco...
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Universiti Kebangsaan Malaysia
2015
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Online Access: | http://journalarticle.ukm.my/8966/1/12_Khairiah_Haji_Badri.pdf http://journalarticle.ukm.my/8966/ http://www.ukm.my/jsm/malay_journals/jilid44bil6_2015/KandunganJilid44Bil6_2015.html |
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my-ukm.journal.89662016-12-14T06:48:34Z http://journalarticle.ukm.my/8966/ A mini scale batch reactor for the production of palm‑based polyol Khairiah Haji Badri, Muhammad Syukri Ngah, An investigation on a batch production of palm kernel oil polyol (PKO-p) was conducted via esterification and condensation. The process design was thoroughly studied as a preliminary step for future upscaling. The process variables included necessity of vacuum pump, controlling of heating rate, recording the production time, nitrogen gas flow and agitator speed. About 250 mL PKO-p was successfully synthesized within 3 h. Vacuum pressure was applied to haul out moisture from the system. The control of heating rate and production time are vital to avoid sudden oxidation. Universiti Kebangsaan Malaysia 2015-06 Article PeerReviewed application/pdf en http://journalarticle.ukm.my/8966/1/12_Khairiah_Haji_Badri.pdf Khairiah Haji Badri, and Muhammad Syukri Ngah, (2015) A mini scale batch reactor for the production of palm‑based polyol. Sains Malaysiana, 44 (6). pp. 861-867. ISSN 0126-6039 http://www.ukm.my/jsm/malay_journals/jilid44bil6_2015/KandunganJilid44Bil6_2015.html |
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An investigation on a batch production of palm kernel oil polyol (PKO-p) was conducted via esterification and condensation. The process design was thoroughly studied as a preliminary step for future upscaling. The process variables included necessity of vacuum pump, controlling of heating rate, recording the production time, nitrogen gas flow and agitator speed. About 250 mL PKO-p was successfully synthesized within 3 h. Vacuum pressure was applied to haul out moisture from the system. The control of heating rate and production time are vital to avoid sudden oxidation. |
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Khairiah Haji Badri, Muhammad Syukri Ngah, |
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Khairiah Haji Badri, Muhammad Syukri Ngah, A mini scale batch reactor for the production of palm‑based polyol |
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Khairiah Haji Badri, Muhammad Syukri Ngah, |
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Khairiah Haji Badri, |
title |
A mini scale batch reactor for the production of palm‑based polyol |
title_short |
A mini scale batch reactor for the production of palm‑based polyol |
title_full |
A mini scale batch reactor for the production of palm‑based polyol |
title_fullStr |
A mini scale batch reactor for the production of palm‑based polyol |
title_full_unstemmed |
A mini scale batch reactor for the production of palm‑based polyol |
title_sort |
mini scale batch reactor for the production of palm‑based polyol |
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Universiti Kebangsaan Malaysia |
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2015 |
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http://journalarticle.ukm.my/8966/1/12_Khairiah_Haji_Badri.pdf http://journalarticle.ukm.my/8966/ http://www.ukm.my/jsm/malay_journals/jilid44bil6_2015/KandunganJilid44Bil6_2015.html |
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